A kind of treatment method of unsaturated polyester waste water
A treatment method, polyester wastewater technology, applied in the field of unsaturated polyester wastewater treatment, can solve the problems of increased wastewater treatment operating costs, changes in sludge properties, uneconomical and practical, etc., to achieve good economic and environmental benefits, process Short, low energy cost effect
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Embodiment 1
[0024] The treatment method of the invention is used to treat the unsaturated polyester resin wastewater produced in the polycondensation stage. The content of organic matter in polyester wastewater is about 15 wt%, of which the content of dihydric alcohol is about 11.2~11.8 wt%, the content of phthalic anhydride and maleic anhydride is 2.5~2.7 wt%, and other light organic matter is 0.3~1.2 wt% (The following examples and comparative examples adopt the same polyester waste water). The unsaturated polyester waste water is firstly treated by rectification. The primary condenser is a stainless steel condensing tower with a processing capacity of 10L / h. It is equipped with a condensing plate and a reflux system. The tower is filled with PVC packing. The rectification condition is the temperature inside the tower. 100±2°C, the temperature of the condensate at the top of the tower is 80°C, the batch processing is 10L / time, the residence time is 1h, and the liquid phase reflux ratio ...
Embodiment 2
[0026] The treatment method of the invention is used to treat the unsaturated polyester resin wastewater produced in the polycondensation stage. The unsaturated polyester waste water is firstly treated by rectification. The primary condenser is a stainless steel condensing tower with a processing capacity of 10L / h. It is equipped with a condensing plate and a reflux system. The tower is filled with PVC packing. The rectification condition is the temperature inside the tower. 100±2°C, the temperature of the condensate at the top of the tower is 75°C, the batch processing is 10 L / time, the residence time is 1.5h, and the liquid phase reflux ratio is 5:1. Dosing NaOH and Na in the treated effluent 2 CO 3Adjust the pH value of the wastewater to 6.0, the mass ratio of the two is 5:1, and add 50g of feces per L of wastewater to supplement nitrogen and phosphorus (that is, COD:N:P is about 70:5:1). After fully mixing, the wastewater enters the high-temperature anaerobic treatment. ...
Embodiment 3
[0028] On the basis of Example 2, ammonium chloride and potassium dihydrogen phosphate were added according to COD:N:P=70:5:1 to supplement N and P nutrient salts. Other treatment conditions were the same as in Example 2, and the COD of the effluent was measured. 196 mg / L, BOD 5 It was 88.6 mg / L, ammonia nitrogen was 18.5 mg / L, and volatile phenol was 5.7 mg / L.
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